A New Reactor Concept for Efficient Solar-Thermochemical Fuel Production

We describe and analyze the efficiency of a new solar-thermochemical reactor concept, which employs a moving packed bed of reactive particles produce of H2 or CO from solar energy and H2O or CO2. The packed bed reactor incorporates several features essential to achieving high efficiency: spatial separation of pressures, temperature, and reaction products in the reactor; solid–solid sensible heat recovery between reaction steps; continuous on-sun operation; and direct solar illumination of the working material. Our efficiency analysis includes material thermodynamics and a detailed accounting of energy losses, and demonstrates that vacuum pumping, made possible by the innovative pressure separation approach in our reactor, has a decisive efficiency advantage over inert gas sweeping. We show that in a fully developed system, using CeO2 as a reactive material, the conversion efficiency of solar energy into H2 and CO at the design point can exceed 30%. The reactor operational flexibility makes it suitable for a wide range of operating conditions, allowing for high efficiency on an annual average basis. The mixture of H2 and CO, known as synthesis gas, is not only usable as a fuel but is also a universal starting point for the production of synthetic fuels compatible with the existing energy infrastructure. This would make it possible to replace petroleum derivatives used in transportation in the U.S., by using less than 0.7% of the U.S. land area, a roughly two orders of magnitude improvement over mature biofuel approaches. In addition, the packed bed reactor design is flexible and can be adapted to new, better performing reactive materials.

A New Reactor Concept for Efficient Solar-Thermochemical Fuel Production

We describe and analyze the efficiency of a new solar-thermochemical reactor concept, which employs a moving packed bed of reactive particles produce of H-2 or CO from solar energy and H2O or CO2. The packed bed reactor incorporates several features essential to achieving high efficiency: spatial separation of pressures, temperature, and reaction products in the reactor; solid-solid sensible heat recovery between reaction steps; continuous on-sun operation; and direct solar illumination of the working material. Our efficiency analysis includes material thermodynamics and a detailed accounting of energy losses, and demonstrates that vacuum pumping, made possible by the innovative pressure separation approach in our reactor, has a decisive efficiency advantage over inert gas sweeping. We show that in a fully developed system, using CeO2 as a reactive material, the conversion efficiency of solar energy into H-2 and CO at the design point can exceed 30%. The reactor operational flexibility makes it suitable for a wide range of operating conditions, allowing for high efficiency on an annual average basis. The mixture of H-2 and CO, known as synthesis gas, is not only usable as a fuel but is also a universal starting point for the production of synthetic fuels compatible with the existing energy infrastructure. This would make it possible to replace petroleum derivatives used in transportation in the U. S., by using less than 0.7% of the U. S. land area, a roughly two orders of magnitude improvement over mature biofuel approaches. In addition, the packed bed reactor design is flexible and can be adapted to new, better performing reactive materials.

Enzymatic Activity of Soybean Lipoxygenase-1 on Linoleoyl-Derivatized Agarose

Soybean lipoxygenase-1 (SBLO-1) catalyzes the oxygenation of linoleic acid to form 13(S) and 9(R) hydroperoxides. The manner in which substrates bind to the lipoxygenase family of enzymes is not known. It is believed fatty acid substrates may bind either with the aliphatic end first or with the carboxylate group facing the interior of the protein. This thesis tested a potential methyl-end first substrate binding mechanism by studying the activity of SBLO-1 to oxygenate immobilized linoleoyl residues attached to an insoluble polymer. Linoleic acid was attached to aminohexyl agarose in the presence of N-(3- dimethylaminopropyl)-N’-ethylcarbodiimide hydrochloride (EDC) and Nhydroxysuccinimide (NHS). The concentration of the covalently attached residues was facilitated by enriching linoleic acid with a small amount of the radioactive 14C-isotope. Functionalization yields of 3% available primary amines on the resin were obtained. Enzymatic oxygenation of the linoleoyl-residues was verified using the ferrous oxidation in xylenol orange (FOX) assay. Approximately 30% of the attached linoleoyl moieties were converted to hydroperoxides in the presence of SBLO-1. A disulfide-containing cleavable linker, cystamine, was used as part of an improved method to isolate the product in a facile manner. Cystamine was attached to NHS-activated agarose with approximately 5% overall functionalization yield of available functional groups. 14C-linoleic acid was successfully covalently linked to the cystamine moieties in the presence of EDC and NHS. The FOX assay verified the enzymatic oxygenation of the linoleoyl residues attached to cystamine-derivatized agarose. The isolation of the peroxide product was attempted in a series of extractions in organic solvents. The product was analyzed using GC/MS which did not show a new peak indicative of product. Further work is needed to successfully analyze the stereoand regiochemistry of the oxygenated product. The presence of the peroxides in this study indicated the linoleoyl residues behave as substrates of SBLO-1. It is unknown how bulky substrates bind to the active site; however, it is difficult to rationalize a carboxylate group-first binding mode. Discovery of the 13(S)-hydroperoxide product on the linoleoyl-agarose would support the claim of a potential methyl-end first binding mechanism.